Separation of cobalt from nickel in ammoniacal solutions using 8-hydroxyquinolines

Claim 2

Method of separating dissolved cobalt value from dissolved nickel value from a pregnant aqueous ammoniacal solution, containing sufficient dissolved ammonia to maintain the nickel and cobalt dissolved in the aqueous solution, having a pH in the range of at least about 8.5 and comprising at least about 7 grams/liter dissolved ammonium halide measured as ammonium ion; the process comprising: contacting the nickel- and cobalt-containing aqueous solution with an organic liquid ion exchange medium comprising an ion exchange agent selected from the group consisting of 7-hydrocarbon-substituted-8-hydroxyquinolines, while maintaining the aqueous solution at a pH of at least about 8.5, to form an organic extract phase containing the cobalt value and an aqueous phase depleted in cobalt value; and separating the organic extract phase from the aqueous phase; whereby cobalt is preferentially extracted into the organic extract phase.

Claim 3

The method of claim 1, wherein the halide is chloride.

Claim 4

The process of claim 2, wherein the pregnant aqueous solution is maintained at a pH in the range of from about 9.1 to about 9.4, when it is in contact with the liquid ion exchange medium.

Claim 5

The method of claim 1, comprising in addition stripping the cobalt value from the organic extract by contacting the organic extract with an acid solution having a concentration at least 6 Normal in hydrogen ion and chloride ion.

Claim 6

The method of claim 1, wherein the 7-hydrocarbon-substituted-8-hydroxyquinoline is substituted by a substituent selected from the group consisting of alkylbenzyl groups and beta-alkenyl groups, containing from about 12 to about 18 carbon atoms.

Claim 7

The method of claim 1, wherein the liquid ion exchange medium comprises a solution of the ion exchange agent in a water-immiscible organic hydrocarbon liquid.

Claim 8

The method of claim 1, wherein the nickel and cobalt values are present in the pregnant aqueous solution as the halides.

Claim 9

The process of claim 1, wherein the pregnant aqueous solution is maintained at a pH of at least about 9 when it is in contact with the liquid ion exchange medium.

Claim 10

The process of claim 1, wherein the pregnant aqueous solution is maintained at a pH in the range of from about 9 to about 10, when it is in contact with the liquid ion exchange medium.

Claim 11

The process of claim 1, wherein the liquid ion exchange medium comprises a solvent which is immiscible with water, but is a solvent for the extracting agent.

Claim 12

The process of claim 10, wherein the solvent is an organic liquid.

Claim 13

The method of claim 1, wherein the nickel and cobalt values are present in the pregnant aqueous solution as chlorides.

Claim 14

The process of claim 12, wherein the pregnant aqueous solution is maintained at a pH of at least about 9 when it is in contact with the liquid ion exchange medium by the substantially continuous addition of ammonia during the period the aqueous solution is in contact with the organic medium.

Claim 15

The process of claim 1, wherein the ammonium halide is present in a concentration of at least about 12 gm/1, measured as ammonium ion.

Claim 16

Method of separating dissolved cobalt value from dissolved nickel value from a pregnant aqueous ammoniacal solution, containing sufficient dissolved ammonia to maintain the nickel and cobalt dissolved in the aqueous solution, having a pH in the range of at least about 9, and comprising dissolved ammonium ion and chloride ion, representing an ammonium chloride concentration of at least about 38 grams/liter, the process comprising: contacting the nickel- and cobalt-containing aqueous solution with an organic liquid ion exchange medium comprising an ion exchange agent selected from the group consisting of 7-hydrocarbon-substituted-8-hydroxyquinolines, the hydrocarbon group having at least about eight carbon atoms, while maintaining the aqueous solution at a pH of at least about 9 to form an organic extract phase containing the cobalt value and an aqueous phase depleted in cobalt value, and separating the organic extract phase from the aqueous phase; whereby cobalt is preferentially extracted into the organic extract phase.

Claim 17

Method of separating dissolved cobalt value from dissolved nickel value from a pregnant aqueous ammoniacal solution, containing sufficient dissolved ammonia to maintain the nickel and cobalt dissolved in the aqueous solution, having a pH in the range of at least about 9, and comprising dissolved ammonium ion and chloride ion, representing an ammonium chloride concentration of at least about 38 grams/liter, the process comprising: contacting the nickel- and cobalt-containing aqueous solution with an organic liquid ion exchange medium comprising an ion exchange agent selected from the group consisting of 7-hydrocarbon-substituted-8-hydroxyquinolines, the hydrocarbon group having at least about eight carbon atoms, while maintaining the aqueous solution at a pH of at least about 9 to form an organic extract phase containing the cobalt value and an aqueous phase depleted in cobalt value, and separating the organic extract phase from the aqueous phase; whereby cobalt is preferentially extracted into the organic extract phase.

Claim 18

The process of claim 15, wherein the pH of the aqueous solution is maintained in the range of from about 9 to about 10.

Claim 19

The process of claim 16, wherein the nickel and cobalt values are present in the aqueous solution as the chlorides.

Claim 20

Method of obtaining cobalt value substantially free from nickel value from a pregnant aqueous ammoniacal solution, comprising dissolved nickel, cobalt and copper value, and containing sufficient dissolved ammonia to maintain the nickel and cobalt dissolved in the aqueous solution, the pregnant aqueous solution having a pH in the range of at least about 9, and comprising dissolved ammonium ion and chloride ion, representing an ammonium chloride concentration of at least about 20 grams/liter, the process comprising: contacting the pregnant aqueous solution with an organic liquid ion exchange medium comprising an ion exchange agent selected from the group consisting of 7-hydrocarbon-substituted-8-hydroxyquinolines while maintaining the aqueous solution at a pH of at least about 9, to form an organic extract phase containing the cobalt value and the copper value and an aqueous phase depleted in cobalt and copper value; separating the organic extract phase from the aqueous phase; contacting the organic extract phase with a weakly acid aqueous solution containing sufficient amount of hydrogen ions to selectively exchange the copper from the organic phase, to form an aqueous phase containing the copper value and an organic phase depleted in copper value; and separating the aqueous phase from the organic phase; whereby cobalt is obtained in the organic phase.

Claim 21

Method of obtaining cobalt value substantially free from nickel value from a pregnant aqueous ammoniacal solution, comprising dissolved nickel, cobalt and copper value, and containing sufficient dissolved ammonia to maintain the nickel and cobalt dissolved in the aqueous solution, the pregnant aqueous solution having a pH in the range of at least about 9, and comprising dissolved ammonium ion and chloride ion, representing an ammonium chloride concentration of at least about 20 grams/liter, the process comprising: contacting the pregnant aqueous solution with an organic liquid ion exchange medium comprising an ion exchange agent selected from the group consisting of 7-hydrocarbon-substituted-8-hydroxyquinolines while maintaining the aqueous solution at a pH of at least about 9, to form an organic extract phase containing the cobalt value and the copper value and an aqueous phase depleted in cobalt and copper value; separating the organic extract phase from the aqueous phase; contacting the organic extract phase with a weakly acid aqueous solution containing sufficient amount of hydrogen ions to selectively exchange the copper from the organic phase, to form an aqueous phase containing the copper value and an organic phase depleted in copper value; and separating the aqueous phase from the organic phase; whereby cobalt is obtained in the organic phase.

Claim 24

The method of claim 19, wherein the 7-hydrocarbon-substituted-8-hydroxyquinoline is substituted by a substituent selected from the group consisting of alkylbenzyl groups and beta-alkenyl groups, containing from about 12 to about 18 carbon atoms.